FIELD: chemistry.
SUBSTANCE: invention relates to steam treatment of polymer particles in a steaming apparatus after a polymerisation process. The method includes contacting polymer particles with a counter-current of steam. The flow rate of steam entering said steaming apparatus is continuously maintained proportional to the production rate of said polymerisation process in and the gradient between the temperature (Tout) of the polymer exiting said steaming apparatus and the temperature (Tin) of the polymer entering said steaming apparatus. The rate of formation of polyolefin, said temperature Tout at the output and said temperature Tin at the input are determined. Said flow rate is controlled according to a value calculated using the equation: Fsteam=K·FP·ΔTpolymer, where Fsteam is the flow rate (kg/h) of steam entering the steaming apparatus; FP is the flow rate (kg/h) of polyolefin fed at the top of the steaming apparatus; ΔTpolymer=Tout-Tin (°C); K (°C)-1 is the multiplicative constant of the steam flow rate.
EFFECT: controlling the amount of steam used to steam a polymer in a ratio with the amount of polymer entering the steaming apparatus.
9 cl, 1 dwg, 2 ex
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Authors
Dates
2014-08-20—Published
2009-12-23—Filed